Pulverulent material metering and delivery system and method

ABSTRACT

A metering and delivery system for feeding finely powdered coal to a combustion chamber includes a hopper containing finely ground coal, a vertical feed pipe extends from the hopper and a horizontal metering conduit is connected to the lower end of the feed pipe so that the coal provides a surface of repose in the metering conduit below an air flow opening with a bleed opening being downstream of the air flow opening. A venturi jet housing provides suction on the metering conduit drawing ambient air into the openings to entrain coal for injection by an injector lance into a combustion space. Metering of the coal is provided by inversely operated valves through which ambient air flows to the openings in the metering conduit.

This is a division of application Ser. No. 636,649, filed Dec. 1, 1975.

This invention is in the field of pulverulent material metering andsupply systems and is specifically directed in its preferred embodimentto a solid fuel metering and deliverying system for providing a meteredquantity of comminuted coal or similar solid particle fuel to a kiln,boiler or similar combustion chamber.

One of the reasons that petroleum based fuels have achieved widespreadacceptance and use is the fact that they can be fed to a burner assemblyat a closely controlled rate for achieving optimum performance in theparticular installation in which they are used. While solid fuels suchas coal have substantial advantages in terms of dollar costs per BTU,such advantages have been greatly outweighed by the inability to controlflow in small quantities to the burning area in the accurate mannerachieved by petroleum based systems. This drawback has resulted in theceramic industry relying almost totally upon petroleum based fuels suchas natural gas for the fueling of kilns. Projected shortages of naturalgas and the ever increasing costs of all petroleum based fuels haveresulted in a great need for a fuel delivery and metering system forcoal that can provide the high degree of control necessary in manyindustrial uses such as the ceramic industry in order to avoid the highcost and scarcity of petroleum based fuel. In fact, the need for asatisfactory coal delivery and metering system is particularly criticalin the ceramic industry in which kilns require a large number of smallburners each of which must provide an accurate temperature control in afinite zone in order to provide a satisfactory product and the highprice and likely inavailability of petroleum based fuels in the futurerenders the provision of a satisfactory coal burner system essential tothe survival of the ceramic industry.

Additionally, many other industries such as the chemical, pharmaceuticaland food product industries require means capable of providing accuratequantities of powdered or comminuted materials. The inability to providea continuous metered flow of such materials in small quantitiesfrequently results in such industries having to employ the batch methodof mixing compounds in which the components are weighed and then mixed.The present invention provides simple means which can be used toaccurately provide a metered continuous flow of pulverulent orcomminuted material in a continuous mixing process. The terms"pulverulent" and "comminuted" are used interchangeably throughout thespecification and claims of this application in their broadest sense toinclude any solid powdery type material that is capable of beingfree-flowing. Examples of such materials include finely ground coal,coke, sand abrasive grits, pelletized plastics, flour, cornmeal,pigments, talc, granulated solids such as sugar or salt, organiccompounds and many other materials of like nature which are too numerousto mention.

Therefore, it is the object of this invention to provide a new andimproved pulverulent material delivery and metering system. A furtherobject of the invention is the provision of a new and improved fueldelivery and metering system for feeding controlled quantities of coalor similar solid fuel to a combustion chamber.

Achievement of the objects of this invention is enabled by the preferredembodiment of the invention which includes a source of finely groundpowdered coal comprising a material hopper from the lower end of which avertically extending feed pipe is provided. A horizontal meteringconduit is connected on one end to the lower end of the feed pipe sothat finely ground comminuted coal flows down the feed pipe and into theend of the metering conduit adjacent the lower end of the feed pipe toprovide a surface of repose in the metering conduit. First and secondair induction openings are provided in the upper side of the meteringconduit with the first air induction opening in the metering conduitconsisting of a feed air induction opening positioned above the surfaceof repose of the powdered coal provided in the metering conduit by thegravitational movement of the coal from the infeed pipe. The uppersurface of the powdered coal in the metering conduit has an angle ofrepose of approximately 45° and the feed air hole is immediately abovethis surface. The second air induction opening is a bleed air supply andis provided in the upper surface of the metering conduit immediatelydownstream of the feed air opening for providing a quantity of air intothe metering conduit. Both the feed air induction opening and the bleedair induction opening permit the ambient air to flow into the meteringconduit for a purpose to be described hereinafter.

The feed air opening and the bleed air opening are both connected topipe risers on which interconnected feed air and bleed air controlvalves are mounted. A manually operable inverse adjustment meansconnects the feed air valve and the bleed air valve to adjust theirdegree of opening in an inverse manner. In other words, when the feedair valve is moved toward an open condition, the bleed air valve ismoved toward a closed condition by a like or proportional amount. It isthe foregoing inverse operational relationship of the feed air valve andthe bleed air valve which enables a highly accurate metering of thecomminuted coal particles.

The downstream end of the metering conduit is connected to a venturihousing in which an air injector is provided for creating a pressuredrop through the feed air valve, the bleed air valve and the meteringconduit so that ambient air flows through the feed air valve to engagethe coal surface of repose and entrain coal particles therefrom. Themixture of air and coal particles is sprayed by an injector into thekiln or other area in which the combustion is to take place. The amountof air injected by the venturi serves to vary the velocity of the fueland air mixture through the injector to vary the depth of flamepenetration in the combustion chamber and also serves to increase themaximum feed rate capacity of the system. However, the metering of thefuel is accomplished by the operation of the feed air control valve andthe bleed air control valve with maximum feed rate occurring when thebleed air control valve is completely closed and the feed air controlvalve is completely open. It is then possible to vary the fuel flow in alinear manner by operation of the fuel control valve.

A better understanding of the manner in which the preferred embodimentof the invention accomplishes the objects of the invention will beachieved when the following written discussion is considered inconjunction with the appended drawings in which:

FIG. 1 is a perspective flow diagram of the preferred embodiment withportions removed for clarity;

FIG. 2 is a bisecting sectional view of the feed metering portion of thepreferred embodiment; and

FIG. 3 is a bisecting sectional view of the venturi and injectorportions of the preferred embodiment.

The preferred embodiment of the invention illustrated in the drawings isdirected to a fuel supply system for a kiln or the like and includes afeed hopper 10 in which a supply 11 of pulverized coal is provided. Ithas been found that minus 8 mesh coal of less than 3% moisture contentprovides highly satisfactory operation with the pulverized coal flowfrom the hopper flowing through a ball valve 12 which can be closed by ahandle 13 when necessary to discontinue the feed of coal from the hopperfor enabling repair or other maintenance operations on the remainder ofthe system.

A vertically extending feed pipe 14 has its upper end connected to theball valve 12 and has its lower end connected by a smooth welded rightangle junction to the upstream end of a horizontal metering conduit 16.The infeed pipe 14 and metering conduit 16 are formed of 1 inch blackiron pipe cut and welded together into a smooth right angle elbowdefining their junction so that gravity causes the powdered coal to flowinto the end of conduit 16 and provide a stationary surface of repose 17as shown in FIG. 2.

The metering conduit 16 is provided with a feed air opening 18positioned in its top surface above the surface of repose 17 of the coalas also shown in FIG. 2. A bleed air opening 22 is spaced from the feedair opening 18 with the openings 18 and 22 being respectivelycommunicating with pipe risers 24 and 26 which are welded to themetering conduit 16. A feed air control valve 28 is mounted on the upperend of the pipe riser 24 and a bleed air control valve 30 is mounted onthe upper end of the pipe riser 26 with the opposite sides of the valves28 and 30 being open to the atmosphere.

A manually operable valve interconnection assembly 32 is connectedbetween the valves 28 and 30 for simultaneously opening and closing thegates 28' and 30' of valves 28 and 30 in an inverse manner. In otherwords, operation of the valve interconnection assembly 32 in a directionto open valve 28 will serve to cause closure of valve 30. In likemanner, opening of valve 30 results in the closure of valve member 28.The valves 28 and 30 are gate valves with non-rising valve stems and areof identical construction. A reducer 34 is mounted on the end ofmetering conduit 16 opposite its juncture with the vertical infeed pipe14 with a flexible hose 36 being connected by means of an adapter 38 tothe metering conduit in an obvious manner.

The opposite end of the hose 36 is connected to a venturi housing 40 inwhich a venturi jet 42 is provided as shown in FIG. 3. Venturi jet 42 isconnected by a hose 44 to a source of compressed air consisting of ablower air header 46 connected to a butterfly valve 48 and pipe 50 tothe hose member 44. All flexible hose connections are made by means ofan adapter identical to adapter 38 in an obvious manner. Air injected bythe venturi 42 lowers the pressure in the housing 40 in a well-knownmanner and induces ambient air flow through valve 28 and 30 into conduit16. The jet from venturi 42 and coal powder from the surface 17 andinduced air are directed into the upstream end of an injector lance 52mounted in a lance holder 54 in a wall 56 of a kiln with secondarycombustion air being supplied to the holder by hose 61. The lance holder54 is in the form of a straight pipe closed at the back end except foran axial opening through which the injector lance is inserted. The axialopening serves as a rear support for the lance while a small section ofpipe 63 mounted by a spider arrangement 65 downstream in the lanceholder provides the forward support to keep the lance centered. Anopening is provided near the rear of the lance holder at approximately90° to the axis of the lance and intersecting the lance holder at itsperiphery. The purpose of this opening is to receive secondarycombustion air from hose 61 which air flows around the lance into thecombustion chamber in a swirling motion and also keeps the lance andlance holder cool.

The compressed air supply system can be a blower or an air compressordepending upon the feed requirements of the particular installation. Inthe preferred embodiment, the system works quite well with the blowercapable of providing pressure no greater than 55 inches of water columndownstream of the butterfly valve 48 with satisfactory operation at apressure as low as 10 ounces per square inch being possible.

The employment of the flexible hose members 36 and 44 is not essentialto the operation of the device; however, the flexibility provided by thehose members permits the injector lance 52 to be positioned as desiredin one of several openings in the kiln wall and to also be easilypositioned axially with respect to the kiln wall.

The injector lance 52 must be of sufficient length as to be capable ofcarrying the fuel mixture through the wall of the kiln to the desiredpoint of injection into the combustion chamber. The lance should be madeof material having sufficient resistance to heat to withstand the hightemperatures generated in the combustion chamber in which it is used.Standard iron, stainless steel, or ceramic tubing are suitable materialsfor the lance in most operations.

In operation, motive air is provided from the header 46 to valve 48,conduit 50 and hose 44 to the venturi nozzle 42 from which it is ejectedinto the lance member 52. Operation of nozzle 42 creates a loweredpressure in the venturi housing 40 which draws air through the valves 28and 30, metering conduit 16 and hose 36 into housing 40.

The air induced through the feed air opening 18 onto the surface ofrepose 17 of the coal engages the minute coal particles and entrainsthem in the air stream at the left end of the metering conduit 16. Thepowdered coal is continuously replenished downwardly through the infeedpipe 14 so that the surface 17 essentially remains in the same positionat all times so as to be impinged upon by the air flowing through theopening 18. Additional air is induced through the bleed air hole 22 withthe bleed air mixing with the air and coal particles and flowing throughthe hose 36 into the venturi housing 40 in an obvious manner. It shouldbe understood that the total amount of air induced through the valves 28and 30 is constant with the only variation being in the ratio of theamount provided by each of the individual valve members. Maximum fuelflow is achieved when the valve 30 is closed and all of the air isinduced via the valve member 28. Minimum flow is obtained when valve 28is closed and the air is induced through the valve 30. Consequently, bymanually adjusting the valve interconnection member 32 or by the use ofautomatic controls, the amount of fuel fed to the injector lance 52 canbe varied accurately in accordance with the particular operation beingperformed.

The amount of air injected by the nozzle 42 remains constant but can beincreased or decreased in order to adjust the feed range of the entireassembly.

There is a linear relationship between the degree of opening of valve 28and the air being induced by the feed air opening 18 and the resultantrate at which the fuel is conveyed away from the surface of repose 17.

Any increase in the flow of motive air through the venturi 42 increasesthe maximum feed rate capability of the system and simultaneouslyincreases the exit velocity of the gas and solid fuel particles from theinjector lance 52. Such an increase in the motive air flow through theventuri does not have any effect whatsoever on the ability of the solidfuel feeder assembly associated with the metering conduit 16 to controlthe amount of solid fuel from a maximum feed rate to a minumum flow ratein a linear manner by operation of the valves 28 and 30 as previouslydiscussed.

It is desirable that the opening 22 be relatively close to the opening18 in order to prevent the occurrence of a buildup or mound of powderedcoal between these two openings under low flow conditions. Moreover, aclose positioning of the bleed air opening 22 to the fuel air opening 18also provides greater linearity in the flow rate variation and valveopening under low flow conditions. In a typical application, pipe 14 andconduit 16 are 1 inch pipe with the spaces between the openings 18 and22 being 4 inches. The risers are approximately 11/2 inches tall and are3/4 inch size as are the gate valves 28 and 30. The hose members are 3/4inch size and the nozzle member 42 consists of a stainless steel pipehaving a 3/8 inch outside diameter and a 0.035 inch thick wall.

Pipe 50 is 3/4 inch size and the air pressure can be varied to anydesired level. In the preferred embodiment using turbo blower air, theair pressure can be varied from zero to 24 ounces. When operating withzero air pressure, a zero amount of fuel would be fed to the injector 52with the device being capable of feeding up to 40 lbs. of coal per hourwhen operating at 24 ounces of pressure. Higher pressures in the samesystem result in a much higher maximum feed rate. 190 Pounds per hourcan be fed with 12 psi compressor air. It should be understood that thedimensions of the parts and the operating pressures can varyconsiderably and it would be possible to provide compressed air to theinlets of the valve members 28 and 30 if desired. The dimensional andoperating variations would depend upon the desired flow rates, thequality of coal being used and the nature of the particular operation.In any event, the inventive device provides a uniquely simple andeffective means for varying the flow of powdered coal to a combustionchamber so as to permit the use of such fuel in low capacity fuelinjection units in operations previously limited to the use of petroleumbased fuels.

Consequently, the present invention meets a long-standing need of thebrick and ceramic industry for means capable of burning coal under closecontrol by the use of a large number of small volume fuel deliverydevices each having a wide range of operation while being easilycontrolled to provide a metered fuel flow at its particular location. Inaddition, use of the metering and delivery system is not limited toburner operations since the system can be used for feeding practicallyany pulverulent material in metered quantities for mixing or otherpurposes.

A particular advantage of the invention is that it is economical tofabricate and maintain since it does not require special equipment andcan be completely fabricated from off the shelf components. Advantagesof operation of the preferred embodiment used as a burner include thefact that the exit velocity of the solid fuel from the injector lancecan be varied to vary the fuel penetration into the combustion chamber.Another advantage of the inventive preferred embodiment resides in thefact that the solid fuel feed rate into the combustion chamber can bevaried over a wide range without affecting the total carrying air usedto delivery the fuel or the exit velocity of the fuel into thecombustion chamber. The device is capable of providing a wide range offuel feed rates while operating under low pressure air supply of between10 to 24 ounces per square inch which makes it possible to operate byuse of a turbo blower air supply as opposed to an expensive compressorsystem. However, the device can be used for high pressure operation ifdesired.

While numerous modifications of the subject invention will undoubtedlyoccur to those of skill in the art, it should be understood that thespirit and scope of the invention is to be limited solely by theappended claims.

We claim:
 1. A method of providing a metered flow of finely powderedcoal into a combustion chamber, said method consisting of the steps ofproviding a surface of repose of said finely powdered coal oriented atapproximately 45° from horizontal, causing an ambient air stream to movesubstantially downwardly to continuously impinge upon said surface ofrepose to entrain coal particles therefrom and conveying said removedcoal particles and the air from said air stream into said combustionchamber.
 2. The method of claim 1 wherein said surface of repose isprovided by permitting the gravitational flow of powdered coal from avertically extending hollow member having a downwardly facing loweropening discharging said powdered coal into an adjacent horizontalhollow metering member positioned below said vertically extending hollowmember.
 3. A method of providing a metered flow of comminuted materialto a desired location, said method consisting of the steps of providinga surface of repose of said comminuted material oriented atapproximately 45° from horizontal, causing an ambient air stream to movesubstantially downwardly to impinge upon said surface of repose toentrain comminuted material therefrom and convey said material to saiddesired location.
 4. The method of claim 3 wherein said surface ofrepose is provided by permitting the gravitational flow of comminutedmaterial from a vertically extending hollow member having a downwardlyfacing lower opening discharging said comminuted material into anadjacent horizontal hollow metering member positioned below saidvertically extending hollow member.
 5. A method of providing anaccurately metered flow of comminuted material, said method includingthe steps of gravitationally feeding said material onto a supportingsurface inside a hollow metering member to form and maintain a surfaceof repose of said comminuted material oriented at an angle greater than30° from horizontal by supplying comminuted material through a hollowmember extending upwardly above said supporting surface so that thecomminuted material flows from a lower end portion of said hollow memberto said suporting surface, continuously directing an air stream toimpinge upon said surface of repose to entrain comminuted materialtherefrom and convey said entrained material along said hollow meteringmember toward said desired location.
 6. The method of claim 5 includingthe providing of a second air stream flowing into said hollow meteringmember at a location downstream of said surface of repose to provideadditional air flow to convey the comminuted material removed from saidsurface of repose.
 7. The method of claim 6 including the step ofvarying the rate at which said comminuted material is delivered to saiddesired location by varying in opposite manner the amount of air flowingin each of said respective air streams while maintaining the totalamount of air flowing in said air streams at a substantially constantvalue.
 8. A method of providing a metered flow of finely powdered coalinto a combustion chamber, said method comprising the steps of providinga surface of repose of said finely powdered coal oriented atapproximately 45° from horizontal by permitting the gravitational flowof powdered coal from a substantially vertically extending hollow memberinto an adjacent substantially horizontal hollow metering member,causing an air stream to move to impinge upon said surface of repose toentrain and remove coal particles therefrom, providing a second airstream flowing into said hollow metering member wherein the flow of saidair streams into said hollow metering member is effected by the loweringof pressure in said hollow metering member to a level less than ambientpressure and the providing of passageways through said hollow meteringmember to the atmosphere so that ambient air flows into said hollowmetering member and conveying said entrained coal particles into saidcombustion chamber.
 9. The method of claim 8 wherein said second ambientair stream is provided between said surface of repose and saidcombustion chamber.
 10. The method of claim 9 including the additionalstep of varying the rate at which said powdered coal is delivered tosaid combustion chamber by simultaneously varying the amount of air ineach of said respective ambient air streams in a reverse manner whilemaintaining the total amount of air flowing through said hollow meteringmember at a substantially constant value.
 11. A method of providing ametered flow of comminuted material to a desired location, said methodcomprising the steps of providing a surface of repose of said comminutedmaterial oriented at approximately 45° from horizontal by permitting thegravitational flow of comminuted material from a vertically extendinghollow member into an adjacent horizontal hollow metering member,causing an ambient air stream to move to impinge upon said surface ofrepose to entrain comminuted material therefrom, providing a secondambient air stream flowing into said hollow metering member wherein theflow of said ambient air streams into said hollow metering member iseffected by the lowering of pressure in said hollow metering member to alevel less than ambient pressure and the providing of passagewaysthrough said hollow metering member to the atmosphere so that ambientair flows into said hollow metering member and conveying said entrainedcomminuted material to said desired location.
 12. The method of claim 11wherein said second ambient airstream is provided to flow into saidhollow metering member at a location between said surface of repose andsaid desired location.
 13. The method of claim 12 including the furtherstep of varying the rate at which said comminuted material is deliveredto said desired location by simultaneously varying the amount of air ineach of said respective ambient air streams in a reverse manner whilemaintaining the total amount of air flowing through said hollow meteringmember at a substantially constant value.
 14. A method of providing ametered flow of finely powdered coal into a combustion chamber, saidmethod consisting of the steps of providing a surface of repose of saidfinely powdered coal oriented at approximately 45° from horizontal bypermitting the gravitational flow of powdered coal from a verticallyextending hollow member into an adjacent horizontal hollow meteringmember, causing an ambient airstream to move in a substantially verticaldirection prior to impingement thereof on said surface of repose toentrain coal particles therefrom, providing a second ambient air streamflowing into said hollow metering member and conveying said removed coalparticles and the air from said ambient air streams into said combustionchamber wherein the flow of said ambient airstreams into said hollowmetering member is effected by the lowering of pressure in said hollowmetering member to a pressure less than ambient pressure and theproviding of passageways through said hollow metering member to theatmosphere so that ambient air flows into said hollow metering member,15. A method of providing a metered flow of comminuted material to adesired location, said method consisting of the steps of providing asurface of repose of said comminuted material oriented at approximately45° from horizontal by permitting the gravitational flow of comminutedmaterial from a vertically extending hollow member into an adjacenthorizontal hollow metering member, causing an ambient airstream to movein a substantially vertical direction prior to impingement thereof onsaid surface of repose at an angle of approximately 45° from saidsurface of repose to entrain comminuted material therefrom, providing asecond ambient air stream flowing into said hollow metering member anddirecting said removal comminuted material and the air from said ambientair streams to said desired location wherein the flow of said ambientairstreams into said hollow metering member is effected by the loweringof pressure in said hollow metering member to a pressure less thanambient pressure and the providing of passageways through said hollowmetering member to the atmosphere so that ambient air flows into saidhollow metering member.
 16. The method of claim 15 including the step ofvarying the ratio of air flow of said ambient air streams to each otherwhile maintaining a relatively constant total flow of air in saidambient air streams.